Catalysts for gas phase production of acetic acid from ethane, processes of making the same and methods of using same

Inactive Publication Date: 2000-07-11
SAUDI BASIC IND CORP SA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

Surprising, the single stage conversion of ethane to acetic acid provides reduced levels of by-products such as carbon monoxide and ethylene. Preferably, the selectivity (%) to carbon monoxide is less than 2%, more preferably less than 1.5%, even more preferably less than 1%, still further preferred less than 0.5% and most preferred about 0%. Preferably, the yield (%) of ethylene is less than 2%, more preferably less than 1.5%, even more preferably

Problems solved by technology

Due to environmental law constraints, carbon monoxide is an undesirable by-product from an industrial point of view.
Acetic acid is conventionally produced by methanol carboxylation using expensive rhodium catalysts in liquid phase homogeneous reactions, which require complicated procedures for the recovery of the catalyst and isolati

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example

Example 1

Mo.sub.1 V.sub.0.628 Pd.sub.2.88E-04 La.sub.1E-05

Ammonium metavanadate (Aldrich Chemicals, Assay=99.0%) in the amount of 6 grams was added to 65 ml of distilled water and heated to 80-90.degree. C. with stirring. Six grams of oxalic acid were added to the above solution. The color of the solution changed from yellowish green to dark brown with a pH between 2 and 2.5 at 80.degree. C. (solution A). Ammonium paramolybdate tetrahydrated (Aldrich Chemicals A.C.S -12054-85-2) in the amount of 14.4 grams was added to 16.7 ml of water and heated to 65.degree. C. to give a colorless solution with a pH between 5.0 and 6.5 (solution B). Solution B was mixed slowly with solution A to give dark blue-green color solution with a pH of 4.22 at 91.degree. C. The 2.5E-03 grams of palladium was added slowly to the gel mixture followed by the required amount of lanthanium nitrate. This dark color combination was stirred vigorously to achieve a homogeneous gel mixture which was then dried slowl...

Example

Example 8 was prepared to check the reproducibility of the catalytic materials.

Example

Example 2

Mo.sub.1 V.sub.0.398 Pd.sub.2.88E-04 La.sub.1.0E-05

The procedure was the same as Example 1 except 3.8 grams of ammonium metavanadate (Aldrich Chemicals, Assay=99.0%) were used.

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Abstract

A mixed metal oxide catalytic system consisting of molybdenum, vanadium, lanthanum and palladium providing higher yields of acetic acid in low temperature single stage oxidation of ethane with molecular oxygen-containing gas without or with reduced production of by-products such as ethylene and CO.

Description

1. Field of the InventionThis invention relates to a catalyst, a method of making the same and catalytic processes for using the same, more specifically to low temperature selective oxidative dehydrogenation of ethane (or mixture of ethane and ethylene) to acetic acid. The invention also relates to single stage catalytic processes using the novel catalyst featuring increased ethane conversions and acetic acid yields at particular process conditions wherein the product stream does not contain significant amounts of side products such as ethylene and CO.2. Description of the Related ArtSeveral publications are referenced in this application. These references describe the state of the art to which this invention pertains, and are incorporated herein by reference.Due to environmental law constraints, carbon monoxide is an undesirable by-product from an industrial point of view. Furthermore, the separation of ethylene from ethane has a great impact on the process economics of ethane oxid...

Claims

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Application Information

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IPC IPC(8): B01J23/648B01J23/54B01J23/652C07C51/16C07C51/215
CPCB01J23/6482B01J23/6525C07C51/215C07C53/08B01J2523/00B01J2523/3706B01J2523/55B01J2523/68B01J2523/824Y02P20/582
Inventor KARIM, KHALIDAL-HAZMI, MOHAMMAD H.KHAN, ASAD
Owner SAUDI BASIC IND CORP SA
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